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A Pore Scale Model For the Transport Phenomena in the Catalyst Layer of a PEM Fuel Cell

机译:PEM燃料电池催化剂层中传输现象的孔尺度模型

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In a proton exchange membrane fuel cell (PEMFC), the catalyst layer is a porous medium made of carbon-supported catalysts and solid electrolyte, and has a thickness in the order of 10 μm. Within this layer, complex transport phenomena take place: transport of charged species (H~+, electrons and ionic radicals), non-charged species (gaseous H_2O, O_2, H_2, N_2 and liquid water) and heat transfer occur in their own pathways. Furthermore, phase change of water and physiochemical/electrochemical reactions also take place on phase boundaries. These transport process take place in an intertwined network of materials having characteristic length scale ranging from nano-meters to micro-meters. The objective of the present study is two-fold, i.e., to develop a rigorous theoretical framework based on which the transport in the micro-structural level can be modelled, and to construct a pore scale model that resolves the geometry of the phases (carbon, ionomer and gas pores) for which direct numerical simulation can be performed. The theoretical framework is developed by employing the volume-averaging techniques for multi-phase porous media. The complete set of the conservation equations for all species in all phases are derived and every interfacial transport is accounted. The problem of model closure on the terms in the transport equations is addressed by the pore-scale model reported in the present study. A 3-D pore-scale model is constructed by a solid model that consists of packing spherical carbon particles and simulated ionomer coating on these carbon aggregates. The index system of the pore-scale model allows easy identification of volumetric pathway, interfaces and triple phase boundaries. The transport of charged and non-charged species is simulated by solving the equations based on first principle in the entire representative element volume (REV) domain. The computational domain contains typically several million cells and a parallelized, iterative solver, GMRES, is employed to solve the coupled transport with complex geometries. Computational results based on the pore-scale model show that the effective transport properties of the species are strongly affected by the micro-structure, e.g. morphology and phase-connectivity. Further simulations and investigation on the coupling effects of the transport are underway. Combination of the proposed theoretical framework and pore-scale model will lay a foundation for the construction of multi-scale modelling of the PEMFC catalyst layer. On the one hand, the pore-scale model helps close the macroscopic volume-averaged equations in the framework. On the other hand, the pore-scale model provides a platform to include microscopic or atomistic simulations.
机译:在质子交换膜燃料电池(PEMFC)中,催化剂层是由碳负载的催化剂和固体电解质制成的多孔介质,并且具有约10μm的厚度。在这一层中,发生了复杂的传输现象:带电物质(H〜+,电子和离子自由基)的传输,不带电物质(气态H_2O,O_2,H_2,N_2和液态水)的传输和热传递发生在它们自己的路径中。此外,水的相变和理化/电化学反应也发生在相界上。这些传输过程在相互缠结的材料网络中进行,这些材料网络的特征长度范围从纳米到微米。本研究的目标是双重的,即建立一个严谨的理论框架,以此为基础,可以在微观结构水平上模拟输运,并建立一个可解析相几何结构的孔尺度模型(碳,离聚物和气孔),可以对其进行直接数值模拟。该理论框架是通过采用体积平均技术为多相多孔介质开发的。得出了所有物种在所有阶段的完整守恒方程组,并考虑了每种界面迁移。本研究报道的孔尺度模型解决了运输方程中的模型闭合问题。通过实体模型构建3-D孔尺度模型,该模型由填充球形碳颗粒和在这些碳聚集体上的模拟离聚物涂层组成。孔尺度模型的指标系统可轻松识别体积路径,界面和三相边界。通过在整个代表元素体积(REV)域中基于第一性原理求解方程,可以模拟带电和不带电物质的传输。计算域通常包含数百万个单元,并采用并行的迭代求解器GMRES来求解具有复杂几何形状的耦合传输。基于孔尺度模型的计算结果表明,物种的有效运输特性受到微观结构的强烈影响,例如形态和相连接性。有关运输耦合效应的进一步模拟和研究正在进行中。所提出的理论框架和孔尺度模型的结合将为PEMFC催化剂层的多尺度建模的构建奠定基础。一方面,孔尺度模型有助于在框架中关闭宏观体积平均方程。另一方面,孔隙尺度模型提供了一个包含微观或原子模拟的平台。

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